Asphalt compositions with sulfur modified polyvinyl acetate (PVAc)

Provided is an asphalt composition that includes a sulfur modified polymer composition and method of making same. The inclusion of 50% by weight sulfur, or greater, into the polymer composition results in a composition that is softer and having an increased melting point, relative to the unmodified polymer composition.

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Description

This application claims priority to U.S. provisional application 61/596,050, filed on Feb. 7, 2012, the disclosure of which is incorporated herein by reference in its entirety.

FIELD OF THE INVENTION

This invention relates to asphalt compositions containing asphalt and modified polyvinyl acetate polymers. More particularly, this invention relates to asphalt compositions containing asphalt and sulfur modified polyvinyl acetate polymers having improved properties relative to unmodified polyvinyl acetate polymers.

BACKGROUND OF THE INVENTION

Sulfur is a co-product of oil and gas production that is produced in ever increasing quantities. For example, sulfur is currently produced at a rate of approximately 10,000 tons/day in Saudi Arabia. The rate of production is expected to increase to 12,000 tons/day in a few years. Although sulfur is a vital resource that is useful for the manufacture a myriad of products, the abundance of sulfur has resulted in worldwide reduction of its price. As worldwide sulfur supplies increase, the storage of the sulfur will present an environmental hazard. New uses of sulfur present one solution to the problem of storing the vast quantities of sulfur.

Previous studies relating to the degradation of PVAc in vacuum using TGA revealed a two stage decomposition. The first mass loss commenced at about 250° C. and continued to about 375° C., after which an inflexion preceded the second and final mass loss that ultimately led to complete decomposition of the polymer. The first mass loss stage was assigned mainly to the release of acetic acid and simultaneous formation of double bonds in the polymer backbone. The formation of both acetic acid and trans-vinylene species have been explained by comparison with pyrolytic cis or syn elimination of low molar mass ester model compounds. It was found that the addition of free radical inhibitors did not prevent elimination of acetic acid. However, previously studies also showed the formation of several volatile products using free radical mechanisms. It has also found that the acetic acid generated has a catalytic effect on degradation. This behavior has been compared to the catalytic effect of HCl on PVC.

Prior investigations have been conducted into inert and oxidative thermal degradation mechanism of PVAc and EVA copolymers using semi-crystalline and amorphous EVA having a VA content in the polymer backbone ranging from about 9 to 73% by weight. More specifically, EVA emulsions of Airflex EN 1035 and Airflex BAF 60 (55 and 60% solids in water, respectively) from Air Products containing 73 and 60% by weight vinyl acetate were utilized. The thermal study was performed over a temperature range of about 200° C. (to remove water and monomers) to about 600° C. and 650° C. for inert and oxidative conditions respectively. The inert degradation of PVAc as measured using a TGA coupled with mass spectrometry (TGA-MS) showed two degradation steps: the first and most intense step is deacytelation, which occurs between about 300 and 400° C. The end of the first thermal degradation step of PVAc in air has been reported to be around 310° C., corresponding to a loss of 95% of the acetic acid formed in the degradation process. Studies have shown that the major volatile degradation product is acetic acid, with smaller amounts of ketene, water, methane, carbon dioxide and carbon monoxide also being formed. Analysis of the degraded sample at 400° C. shows a highly regular unsaturated material. The second step of degradation involves a dehydrogenation reaction.

Thus, there exists a need to provide a modified polymer having improved properties, such as increased melting point, while at the same time providing a use for excess sulfur. One application for such a modified polymer is a sulfur modified polymer for use in asphalt compositions.

SUMMARY

Generally, an asphalt composition that contains an asphalt and a sulfur modified polymer and method of making same is provided. Specifically, asphalt compositions having an asphalt and sulfur modified polyvinyl acetate polymers are provided. The sulfur modified polymers have increased melting points relative to the unmodified polymer.

In one aspect, an asphalt composition containing asphalt and a sulfur modified polyvinyl acetate polymer composition is provided. The sulfur modified polymer includes a polyvinyl acetate polymer and sulfur, wherein the sulfur is present in an amount up to about 50% by weight.

In certain embodiments, in the sulfur modified polymer, the sulfur is present in an amount between about 10 and 20% by weight. In alternate embodiments, the sulfur is present in an amount between about 20 and 30% by weight. In alternate embodiments, the sulfur is present in an amount between about 30 and 40% by weight. In alternate embodiments, the sulfur is present in an amount between about 40 and 50% by weight. In certain embodiments, at least a portion of the sulfur is present in elemental form. In certain embodiments, the sulfur modified polymer is a sulfur modified polyvinyl acetate polymer and has a melting point that is up to 50° C. greater than the melting point of the unmodified polyvinyl acetate polymer. In certain embodiments, the sulfur modified polyvinyl acetate polymer has a melting point that is between 10° C. and 50° C. greater than the melting point of the unmodified polyvinyl acetate polymer. In certain embodiments, the sulfur modified polyvinyl acetate polymer has a melting point that is between 10° C. and 30° C. greater than the melting point of the unmodified polyvinyl acetate polymer. In certain embodiments, the sulfur modified polyvinyl acetate polymer has a melting point that is between 20° C. and 40° C. greater than the melting point of the unmodified polyvinyl acetate polymer. In certain embodiments, the sulfur modified polyvinyl acetate polymer composition has a melting point that is between 30° C. and 50° C. greater than the melting point of the unmodified polyvinyl acetate polymer.

In certain embodiments, the polyvinyl acetate polymer has a molecular weight of between about 10,000 and 25,000, alternatively between about 25,000 and 75,000, alternatively between about 75,000 and 125,000.

In another aspect, a method for preparing an asphalt composition that contains asphalt and a sulfur modified polymer is provided. The method includes the steps of providing a polyvinyl acetate polymer, wherein the polyvinyl acetate polymer has a melting temperature of less than about 140° C.; and heating the polyvinyl acetate polymer in the presence of elemental sulfur to a temperature of between about 150° C. and 200° C. and mixing the polyvinyl acetate polymer and sulfur such that elemental sulfur is incorporated into the polyvinyl acetate polymer to produce a sulfur modified polyvinyl acetate polymer. The sulfur modified polyvinyl acetate polymer is then mixed with asphalt until the sulfur modified polyvinyl acetate polymer is incorporated into the asphalt.

In certain embodiments, between about 40 and 50% by weight sulfur is incorporated into the sulfur modified polyvinyl acetate polymer. In certain embodiments, between about 50 and 70% by weight sulfur is incorporated into the sulfur modified polyvinyl acetate polymer. In certain embodiments, the polyvinyl acetate polymer and sulfur are mixed for at least about 15 minutes. In certain embodiments, between about 40 and 70% by weight asphalt is incorporated into the sulfur modified polyvinyl acetate polymer. In certain embodiments, the sulfur modified polyvinyl acetate polymer and the asphalt are mixed for at least about 15 minutes.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a stress-strain curve comparing pure polyvinyl acetate and sulfur modified polyvinyl acetate.

FIG. 2 is a thermal analysis curve of sulfur.

FIG. 3 is a thermal analysis curve of a polyvinyl acetate sample.

FIG. 4 is a thermal analysis curve of a second polyvinyl acetate sample.

FIG. 5 is a thermal analysis curve of a sulfur modified polyvinyl acetate sample.

FIG. 6 is a thermal analysis curve of another sulfur modified polyvinyl acetate sample.

FIG. 7 is a thermal analysis curve of another sulfur modified polyvinyl acetate sample.

FIG. 8 is a thermal analysis curve of another sulfur modified polyvinyl acetate sample.

 DETAILED DESCRIPTION OF THE INVENTION

Although the following detailed description contains many specific details for purposes of illustration, it is understood that one of ordinary skill in the art will appreciate that many examples, variations and alterations to the following details are within the scope and spirit of the invention. Accordingly, the exemplary embodiments of the invention described herein and provided in the appended figures are set forth without any loss of generality, and without imposing limitations, on the claimed invention.

In this invention, “asphalt” refers to a solid or nearly solid form of bitumen that can melt upon heating and contains impurities such as nitrogen, oxygen and sulfur.

Polyvinyl Acetate (PVAc) samples of different molecular weights were modified using elemental sulfur. The sulfur modified polyvinyl acetate polymers showed increased resistance to melting (i.e., increased melting point for the modified polymer) and produced a softer polymer than the original, unmodified polyvinyl acetate polymer. In general, polyvinyl acetate polymers were selected that had a melting temperatures of less than about 140° C. In general, the addition and mixing of sulfur was performed at a temperature greater than the melting point of the polyvinyl acetate polymer, for example in the range 150°-200° C. Alternatively, the addition and mixing of sulfur can be performed in the range of about 150-160° C., alternatively between about 160 and 170° C., alternatively between about 170 and 180° C., alternatively between about 180 and 190° C., alternatively between about 190 and 200° C. In general, the temperature at which the sulfur addition and mixing take place is maintained at a temperature that is below the decomposition temperature of the polyvinyl acetate polymer. Sulfur was added to the polyvinyl acetate polymer in amounts up to about 50% by weight of the polymer to produce sulfur modified polyvinyl acetate polymer having significantly different and unexpected mechanical properties, as compared with the pure polymers. In addition to the increase in melting point of the sulfur modified polyvinyl acetate polymer, the addition of sulfur to the polyvinyl acetate polymers also produced a polymer material that was softer and more ductile in comparison with pure polyvinyl acetate polymers and showed no strain hardening like the homopolymer. In certain embodiments, the addition and mixing of sulfur described herein can be used for other polymers having similar melting point ranges.

One advantage of the sulfur modified polyvinyl acetate polymers is that the polymer can then be produced at a highly competitive cost because sulfur is very abundant and much cheaper than the polymer. This allows for the vast quantities of sulfur that are produced as a byproduct of oil and gas production to be utilized, thereby eliminating environmental concerns associated with the storage thereof.

In certain embodiments, the sulfur modification of the polyvinyl acetate polymer can result in an increase in the melting points of the polymers by more than 40° C. In certain embodiments, the addition of sulfur to the polymer results in an increase of the melting point of the polymer by about 10° C., alternatively by about 20° C., alternatively by about 30° C. In certain embodiments, the addition of sulfur to the polymer results in an increase of the melting point of the polymer by about 50° C., or greater.

Further, the sulfur modified polyvinyl acetate polymer differs from that of the unmodified polyvinyl acetate polymer because the sulfur composition becomes part of the polymer structure and at high content. The sulfur modified polymers can be used in adhesives and as an oil resistant polymer. In certain embodiments, the sulfur modified polymers finds use as an additive for asphalt compositions. In alternate embodiments, the sulfur modified polymer finds use for use in crack repair of concrete structures and asphalt pavement.

In addition to improving the melting properties of the polymer material, the addition of sulfur to the polymer produces a material that is useful as an asphalt additive, such that the performance grade (PG) of asphalt can be improved. Asphalt is another product of the petroleum refining process. Various materials can be combined with asphalt for the preparation of a wide variety of materials, from adhesives to road materials. In certain embodiments, polymers can be added to asphalt to provide improved properties, such as improved performance grade.

The Strategic Highway Research Program (SHRP) PG binder specification (AASHTO MP1-98) was implemented to determine the performance grades of certain modified asphalt binders. The PG system considered asphalt binder as a linear viscoelastic material whose properties change with temperatures and loading times. The SHRP binder characterization test procedures include Dynamic Shear Rheometer (DSR), and Bending. Beam Rheometer (BBR). The parameters obtained from DSR test are used to measure asphalt binder resistance to rutting at high ambient temperatures and fatigue cracking due to traffic loading at intermediate service temperatures, and include the following: Complex shear modulus, (G*=peak stress/peak strain); Phase angle, δ (defined as the phase difference between stress and strain); shear storage modulus, (G′=G*cos δ); shear loss modulus, (G″=G*sin δ); and G*/sin δ.

EXAMPLES

Polyvinyl acetate polymers obtained from Scientific Polymer Products, Ontario, N.Y., USA were used as received. The technical specifications of the polymers are provided in Table 1. Elemental sulfur (99.9% purity) from Saudi Aramco was used.

TABLE 1 Characterization of Polymers. Resin Product # Class of Polymer Manufacturer Tm, ° C. VA, % Mw Density g/cm3 PVAc1 1019 Polyvinyl acetate Scientific Polymer  70* 100 15000 1.1700 PVAc2 347 Polyvinyl acetate Scientific Polymer 105* 100 100000 1.1700 *softening temperature as reported by the product data sheet

The sulfur modified polymers (SMP) were prepared in a Haake PolyDrive melt blender. In an effort to include as much sulfur as possible into the polymer blend, the composition of sulfur used was 50% and 70% by weight. The Haake PolyDrive melt blender is designed for use as a computer-controlled torque rheometer. The pure polymer and sulfur-polymer blends were mixed in the melt blender at 100 rpm for various different blend times. The blender thus acts as a batch stirred reactor with a constant volume. Samples were collected following the mixing process and analyzed by different techniques. Blends of PVAc1/sulfur, containing 50% by weight sulfur were prepared in the melt blender. The blending time, Tm, was 10 minutes and reaction temperature was 200° C. This sample preparation procedure was repeated for blend times, Tm=15 min and 20 min. The above procedure was also repeated using PVAc2 and PVAc1. The samples were prepared at different processing times to investigate the effect of processing time on total sulfur content and the amount of bonded sulfur in the SMP. Estimating the amount of total sulfur in the SMP was possible, however estimating the amount of bonded sulfur in the SMP was unsuccessful. Three blend samples (PVAc1/S (50:50); PVAc1/S (30:70) and PVAc2/S (50:50)) were prepared at processing time of 15 min.

A Vario EL elemental analyzer was used to determine the amount of free sulfur present in SMP. The thermal behavior of the pure resins and blends was determined by means of a TA Q1000 DSC. Samples of 7-10 mg were weighed and sealed in aluminum hermetic pans. Melting temperature measurements were performed by heating samples from room temperature to 250° C. at a heating rate of 10° C./min, with a nitrogen purge gas at a flow rate of about 50 mL/min.

TABLE 2 Mechanical Properties of pure and sulfur modified PVAc Property Pure PVAc PVAc + 50% Sulfur Young's Modulus (MPa) 4.31 1.93 Yield Strength (MPa) 21.51 9.05 % Elongation 68.32 30.84

As shown in Table 2, the addition of sulfur to the polyvinyl acetate resulted in a softer material which demonstrated a drop in mechanical properties as the material started to elongate freely after the yield point (no strain hardening behavior). Table 3 provides the results of analysis technique used to estimate total sulfur present in the SMP. The results closely match the actual amount of sulfur used in the blending process. The SMP is not soluble in hot alcohol or hot acetone.

TABLE 3 % of Sulfur (S) in SMP. S, Temp Total Measured No. Sample ID Mw wt. % Time (min) (° C.) Sulfur (wt. %) 1 PVAc1 15000 50 10 200 55.9 2 PVAc1 15000 50 15 200 53.4 3 PVAc1 15000 50 20 200 51.1 4 PVAc2 100000 50 10 200 47.3 5 PVAc2 100000 50 15 200 49.8 6 PVAc2 100000 50 20 200 50.4 7 PVAc1 15000 70 10 200 71.0 8 PVAc1 15000 70 15 200 69.5 9 PVAc1 15000 70 20 200 71.6 10 PVAc2 100000 70 10 200 73.0 11 PVAc2 100000 70 15 200 70.9 12 PVAc2 100000 70 20 200 65.8

FIGS. 2-8 show the DSC melting thermograms of the pure sulfur, PVAc and several of the sulfur modified polyvinyl acetate blends. Pure sulfur exhibited two distinct peaks at approximately 106° C. and 122° C., as shown in FIG. 2, indicating the melting transition of two crystal constituents. Pure PVAc1 (Mw=15000) shown in FIG. 3 shows a gradual softening transition as the temperature increases up to 150° C. Pure PVAc2 (Mw=100000) shown in FIG. 4 display a strong peak at around 40° C. and a weak peak around 160° C. It is not believed that the weak peak corresponds to the thermal degradation of PVAc, which is believed to occur at above 227° C. FIG. 5 shows the DSC thermograms of several different blends of PVAc1/sulfur (having 50:50 compositions) prepared at different blending times. A single melting peak around 120° C. for each of the blends corresponds to the thermogram observed in the pure sulfur indicating the presence of sulfur in each of the blends. As shown in FIG. 6, increasing the sulfur content in the blend results in a similar trend wherein the thermograms of the various polymer blends show similar melting peaks associated with the presence of free sulfur. As shown in FIGS. 7 and 8, the observed peaks correspond to those of sulfur and the pure polyvinyl acetate polymer sample, which may correspond to a new material resulting from the reaction of sulfur and the polymer.

For the PG testing, a special blender having of high shear blade was used to blend the polymer with the asphalt at a blending speed was controlled with a DC motor capable of producing up to 3000 rpm. The temperature was controlled at 140° C. through a heating oil bath. Mixing time was limited to 10 minutes.

The output of bending beam rheometry, which evaluates the low temperature creep stiffness properties of the asphalt binders, are creep stiffness (S) and creep rate (m-value). The creep rate is the slope of log stiffness versus log loading time at 60-second time. These parameters are important to determine asphalt binder resistance to thermal cracking due to temperature drop. All parameters were measured on the unaged, Rotational Thin Film Oven (RTFO) aged, and the Pressure Aging Vessel (PAV) aged binder. In addition, the rotation viscosity test was performed on the fresh binder at 135° C. to determine the workability of the asphalt binder.

The result of PG-grading test is shown in Table 4. As shown, the results indicate that all trial blends combinations of sulfur and polymer has resulted in a PG of 70-10 as compared to a PG of 64-10 for plain asphalt, wherein the first number is the average seven-day maximum pavement temperature (in ° C.) and the second number is expected minimum temperature (in ° C.). Thus, asphalt modified with the various different sulfur modified polyvinyl acetate polymers is suitable for use in

TABLE 4 Performance grade of sulfur-PMACM binders. No. Polymer Code Performance Grade (PG) 1 Asphalt 64-10 2 30% PVAc1 + 70% Sulfur 70-10 3 50% PVAc2 + 50% Sulfur 70-10 4 70% PVAc2 + 30% Sulfur 70-10

The methods and compositions provided herein solve several problems that are frequently encountered

Although the present invention has been described in detail, it should be understood that various changes, substitutions, and alterations can be made hereupon without departing from the principle and scope of the invention. Accordingly, the scope of the present invention should be determined by the following claims and their appropriate legal equivalents.

The singular forms “a”, “an” and “the” include plural referents, unless the context clearly dictates otherwise.

Optional or optionally means that the subsequently described event or circumstances may or may not occur. The description includes instances where the event or circumstance occurs and instances where it does not occur.

Ranges may be expressed herein as from about one particular value, and/or to about another particular value. When such a range is expressed, it is to be understood that another embodiment is from the one particular value and/or to the other particular value, along with all combinations within said range.

Throughout this application, where patents or publications are referenced, the disclosures of these references in their entireties are intended to be incorporated by reference into this application, in order to more fully describe the state of the art to which the invention pertains, except when these references contradict the statements made herein.

As used herein and in the appended claims, the words “comprise,” “has,” and “include” and all grammatical variations thereof are each intended to have an open, non-limiting meaning that does not exclude additional elements or steps.

As used herein, terms such as “first” and “second” are arbitrarily assigned and are merely intended to differentiate between two or more components of an apparatus. It is to be understood that the words “first” and “second” serve no other purpose and are not part of the name or description of the component, nor do they necessarily define a relative location or position of the component. Furthermore, it is to be understood that that the mere use of the term “first” and “second” does not require that there be any “third” component, although that possibility is contemplated under the scope of the present invention.

Claims

1. An asphalt composition, the composition comprising:

asphalt;
and a sulfur modified polymer, said sulfur modified polymer comprising a polyvinyl acetate polymer having a melting point; and sulfur, wherein the sulfur is present in the sulfur modified polymer in an amount up to 50% by weight, such that the sulfur modified polymer has an increased melting point as compared to the melting point of the polyvinyl acetate polymer.

2. The asphalt composition of claim 1 wherein the sulfur is present in an amount between about 10 and 20% by weight.

3. The asphalt composition of claim 1 wherein the sulfur is present in an amount between about 20 and 30% by weight.

4. The asphalt composition of claim 1 wherein the sulfur is present in an amount between about 30 and 40% by weight.

5. The asphalt composition of claim 1 wherein the sulfur is present in an amount between about 40 and 50% by weight.

6. The asphalt composition of claim 1 wherein at least a portion of the sulfur is present in elemental form.

7. The asphalt composition of claim 1 wherein the sulfur modified polymer has a melting point that is up to 50° C. greater than the melting point of the polyvinyl acetate polymer.

8. The asphalt composition of claim 1 wherein the sulfur modified polymer has a melting point that is between about 10° C. and 50° C. greater than the melting point of the polyvinyl acetate polymer.

9. The asphalt composition of claim 1 wherein the sulfur modified polymer has a melting point that is between about 10° C. and 30° C. greater than the melting point of the polyvinyl acetate polymer.

10. The asphalt composition of claim 1, wherein the sulfur modified polymer has a melting point that is between about 20° C. and 40° C. greater than the melting point of the polyvinyl acetate polymer.

11. The asphalt composition of claim 1, wherein the sulfur modified polymer has a melting point that is between about 30° C. and 50° C. greater than the melting point of the polyvinyl acetate polymer.

12. The asphalt composition of claim 1, wherein the polyvinyl acetate polymer has a molecular weight of between about 10,000 and 25,000.

13. The asphalt composition of claim 1, wherein the polyvinyl acetate polymer has a molecular weight of between about 25,000 and 75,000.

14. The asphalt composition of claim 1, wherein the polyvinyl acetate polymer has a molecular weight of between 75,000 and 125,000.

15. A method for preparing the asphalt composition of claim 1, the method comprising the steps of:

providing an asphalt;
providing a polyvinyl acetate polymer, wherein the polyvinyl acetate polymer has a melting temperature of less than 140° C.; and
heating the polyvinyl acetate polymer in the presence of elemental sulfur to a temperature of between 150° C. and 200° C. and mixing the polyvinyl acetate polymer and sulfur such that elemental sulfur is incorporated into the polyvinyl acetate polymer to produce a sulfur modified polyvinyl acetate polymer;
mixing the sulfur modified polyvinyl acetate polymer with the asphalt such that the sulfur modified polyvinyl acetate polymer is incorporated into the asphalt.

16. The method of claim 15, wherein between 40 and 50% by weight sulfur is incorporated into the sulfur modified polyvinyl acetate polymer.

17. The method of claim 15, wherein between 50 and 70% by weight sulfur is incorporated into the sulfur modified polyvinyl acetate polymer.

18. The method of claim 15, wherein the polyvinyl acetate polymer and sulfur are mixed for at least 15 minutes.

19. The method of claim 15, wherein the modified polyvinyl acetate polymer and the asphalt are mixed for at least 15 minutes.

20. A method of preparing cracks in asphalt, said method comprising:

applying an asphalt composition of claim 1 to a crack in asphalt.
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Patent History
Patent number: 8721215
Type: Grant
Filed: Feb 7, 2013
Date of Patent: May 13, 2014
Patent Publication Number: 20130202356
Assignee: Saudi Arabian Oil Company (Dhahran)
Inventors: Ibnelwaleed A. Hussein (Dhahran), Mohammed H. Al Mehthel (Dhahran), Hamad I. Al-Abdul Wahhab (Dhahran), Saleh H. Al Idi (Khobar), Mohammed A. Suleiman (Dhahran)
Primary Examiner: Raymond W Addie
Application Number: 13/761,373